Method of increasing enzyme stability and activity for pulp and paper production

a technology of enzyme stability and activity, applied in the field of managing wood pitch, can solve the problems of reducing paper quality, affecting the physical properties of the pulp, and impairing the bonding of fibers to fibers, and achieves the effects of stabilizing the enzyme formulation, speeding up the enzymatic reaction, and enhancing the effect of enzyme formulation

Inactive Publication Date: 2010-07-08
ENZYMATIC DEINKING TECH LLC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0015]A method of treating pitch containing pulp at a higher temperature range than what the esterases allow at normal application temperature or pH has been developed. In one embodiment pitch containing pulp is treated with an effective amount of metal ions selected from the group consisting of aluminum, calcium, magnesium, iron, copper, zinc, titanium and zirconium prior to treatment with a lipolytic enzyme formulation. In another embodiment pitch containing pulp is treated with an effective amount of a cationic polymer. In a more preferred embodiment the pulp is treated with an effective amount of alum. The pulp is treated with an effective amount of a metal ion or cationic polymer effective to increases stability of the enzyme at high temperature and at broad pH ranges of 3-11.
[0018]The wood pulp can be treated for a period of time from about 0.1 to 36 hours, more preferably from about 1.0 to about 12 hours. The addition of metal ions or cationic polymers to the pulp prior to enzyme treatment stabilizes the enzyme formulation and speeds up the enzymatic reactions at high temperature and broader pH range. This enhances the effectiveness of the enzyme formulation in removing extractives such as long chain triglycerides whose conversion is favored thermodynamically at high temperatures. Additionally, the ability of the enzyme formulation to be active at high temperatures decreases the need for adding cooling water prior to enzyme treatment, thus reducing the fresh water use and costs associated with waste waster treatment. Furthermore, the ability of the enzyme formulation to be active at lower pH (as low as 3.0) and higher pH (as high as 10.5) reduces the need for acid or base usage for pH adjustment of pulp stocks prior to enzyme treatment. It makes it possible for enzyme to be added to the locations where the conditions can be too harsh for normal lipolytic enzymes with the use of method described herein. In addition, the chemical costs can be reduced.

Problems solved by technology

Some of the dispersed resin droplets precipitate onto fiber surfaces, impairing fiber to fiber bonding and thereby negatively affecting the physical properties of the pulp.
Dispersed resin which precipitates later in the pulping and papermaking processes can affect paper machine runnability and reduce paper quality, resulting in increased manufacturing costs.
However, those traditional methods have their limitations due to the complexities of pulping and paper making process, particularly when used with recycled paper.
Such treatments, however, can result in increased concentrations of certain pitch components and by-products, such as fatty acids, which would affect machine runnability and product quality.
In fact, one of the major challenges in modern mills with closed-cycle water systems is the removal of lipophilic wood extractives that tend to accumulate in pulping and papermaking systems or circuits because they can no longer be sufficiently purged from the system via the water.
The increasing degree of water closure in mills is leading to an increase in pitch concentrations, which increases the chances of pitch deposition and the discharge of more heavily concentrated pitch-laden waste water.
This makes it more difficult for pulp and papermaking mills to meet state and federal requirements for reducing effluents to meet minimum effluent discharge levels.
However, many mechanical pulping mills are operated at physical and chemical conditions where current commercially available, “normal” enzymes will be deactivated and lose their functions or activities.
Thus the application of normal lipolytic enzymes disclosed in the prior art is limited or even impossible at such high temperatures.
The additional cooling creates many problems, for example, temperature shock to the system, increased fresh water usage, and increased demand of a mill's wastewater treatment capacity.
The addition of cooling water can cause energy loss in a mill.
If the stock consistency is lowered, the mill won't have enough storage space to store pulp stocks.
Therefore, in many mills, lowering the TMP operating temperature to male the enzyme work is simply not viable.
Lipolytic enzymes, being mostly surface-active enzymes, won't work effectively since the TGs and pitch remain solid under temperature ranges where the normal enzymes are active.
Additionally, solubility and miscibility of fatty acids and their corresponding salts increase with temperature.

Method used

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  • Method of increasing enzyme stability and activity for pulp and paper production
  • Method of increasing enzyme stability and activity for pulp and paper production
  • Method of increasing enzyme stability and activity for pulp and paper production

Examples

Experimental program
Comparison scheme
Effect test

example 1

Increased Triglyceride Conversion Kinetics in TMP Pulp

[0044]Materials and Methods

[0045]A newsprint mill TMP pulp stock, collected from secondary refiner accept with no alum addition, was collected. Prior to lab tests, it was mixed well to ensure uniformity of the stock. The stock consistency was determined. Based on the consistency, the stock was diluted to 1.0% consistency, and the pH was adjusted to 5.0-5.2. 100 grams of the 1.0% stock was transferred into each of a series of flasks. The flasks containing stock were conditioned in a water bath at the required temperature for 30 minutes with continuous mixing. Alum solution was added to the stock and mixed for 30 seconds and then enzyme solutions were added to the stock. Pulp samples were collected at reaction time of 20 min to 1.5 hours for testing.

[0046]Results

[0047]FIG. 1 shows the TG conversion results without and with 40# / ton and 80# / ton alum using 0.04% EnzOx® A at 65° C. Total TG conversion as well as the rate of conversion ...

example 2

Increased TG Conversion at a Broader pH Range by Aluminum Addition

[0048]Materials and Methods

[0049]The stock preparation procedure is the same as in Example 1. Two sets of diluted stocks were prepared and pH values were adjusted to pH4.0, 5.0, 6.0, 7.0, 8.0, 9.0 and 10.0, respectively. One set had no alum, while the other set of was treated with 40 lbs / ton of alum. These stocks were then treated with 0.04% of EnzOx® A for 3 hours. The TG content was measured for pulp samples after the treatment.

[0050]Results

[0051]The results are given in FIG. 2. The alum treatment clearly increased the TG conversion by EnzOx® A treatment over the entire pH range tested (4-10). Without alum, only moderate TG conversion was obtained in a narrow range of pH 5-6. Above pH=7, there was essentially no apparent enzyme conversion of TG. With 40# / ton alum addition, the TG conversion was increased to 70-80% with alum treatment. This example demonstrated that aluminum ions could stabilize the lipase enzyme act...

example 3

Increased TG Conversion with Alum Treatment at a Higher Temperature Range with EnzOx® A

[0052]Materials and Methods

[0053]The pulp stock preparation procedure is the same as in Example 1. Two sets of stocks, one with no alum and the other with 30 lbs / ton alum, were prepared. The stocks were then treated with EnzOx® A at 0.04% based on O.D. fibers at different temperatures from 65 to 85° C. for three hours.

[0054]Results

[0055]The results are shown in FIG. 3. Without alum addition, there was no significant TG conversion at above temperature 75° C., indicating that the enzymes were mostly thermally deactivated. In the presence of alum, TG conversion was significantly increased. For instance, at 75° C. TG conversion increased from about 18% without alum to about 82% with 30# / ton alum. It is very obvious that the presence of alum stabilized and protected the enzymes from heat deactivation. The alum addition increased the effective working temperatures for EnzOx® A by about 10° C.

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Abstract

Wood pulp is treated with an esterase formulation in combination with a metal ion or cationic polymer to increase the stability or activity or both of esterase enzymes at high temperature, or at extreme pH ranges of acidic and alkaline conditions. The treatment by esterase together with metals ion or cationic polymer can be used to treat pitch containing pulp at high temperatures prior to, during or after refining of wood chip / pulp, in order to enhance the reduction of pitch problems and facilitate in the manufacture of paper.

Description

FIELD OF THE INVENTION[0001]The present invention is generally in the field of managing wood pitch using enzyme treatment of wood pulp.BACKGROUND OF THE INVENTION[0002]Wood resin is composed of fatty acids and resin acids, triglycerides, steryl esters, and sterols. Wood resins, as well as other extractives such as lignins, pectins, and phenols, are the major components of pitch deposits. During mechanical pulping, the encapsulated resin is liberated from ray parenchyma cells and resin canals. Some of the dispersed resin droplets precipitate onto fiber surfaces, impairing fiber to fiber bonding and thereby negatively affecting the physical properties of the pulp. Dispersed resin which precipitates later in the pulping and papermaking processes can affect paper machine runnability and reduce paper quality, resulting in increased manufacturing costs.[0003]Traditionally, pitch deposits in pulping and paper manufacturing processes have been reduced by seasoning wood logs and chips, and b...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): D21H17/46D21H17/22C08K3/10C08K3/30
CPCD21C9/08D21H17/44D21H17/66D21H21/02D21C9/086D21H11/08D21H17/005D21H17/56
Inventor WANG, XIANG H.MA, JIAN HUAJIANG, CHENGLIANGKAPLAN, HOWARD
Owner ENZYMATIC DEINKING TECH LLC
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